JP2000079462A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JP2000079462A
JP2000079462A JP10251686A JP25168698A JP2000079462A JP 2000079462 A JP2000079462 A JP 2000079462A JP 10251686 A JP10251686 A JP 10251686A JP 25168698 A JP25168698 A JP 25168698A JP 2000079462 A JP2000079462 A JP 2000079462A
Authority
JP
Japan
Prior art keywords
heat transfer
brazing
crest
heat exchanger
holding groove
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP10251686A
Other languages
Japanese (ja)
Inventor
Yasufumi Sakakibara
康文 榊原
Masaharu Ando
正治 安藤
Tadao Kitahara
忠夫 北原
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Maruyasu Industries Co Ltd
Original Assignee
Maruyasu Industries Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Maruyasu Industries Co Ltd filed Critical Maruyasu Industries Co Ltd
Priority to JP10251686A priority Critical patent/JP2000079462A/en
Publication of JP2000079462A publication Critical patent/JP2000079462A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/106Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/105Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being corrugated elements extending around the tubular elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/40Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001Recuperative heat exchangers
    • F28D21/0003Recuperative heat exchangers the heat being recuperated from exhaust gases

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PROBLEM TO BE SOLVED: To stabilize a brazing property and brazing strength of a heat transfer fin by winding a corrugated plate in the direction of a corrugation to form an annular heat transfer fin, bringing the heat transfer fin into contact with a tube wall of a heat exchanger and arranging it and forming a groove which holds a brazing filler metal in the outside of the apex of the corrugation of the heat transfer fin which comes into contact with the tube wall. SOLUTION: A steel strip is formed into a corrugated plate having a prescribed pitch with a press, and a brazing filler metal holding groove 29 is simultaneously formed in the apex 27 of a corrugation which is formed in a flat plate part capable of coming into surface contact with a tube wall. The corrugated plate is bent into an annular shape to form a heat transfer fin 30. The depth of the brazing filler metal holding groove 29 is specified to 0.2-0.8 mm, preferably 0.3-0.5 mm. A paste-like brazing filler metal is filled in the brazing filler metal holding groove 29 or a bar-like brazing filler metal is fit into the groove, the heat transfer fin 30 is inserted into a heat exchanger tube body 28, brazing is executed by being passed through a heating furnace for brazing, and a heat exchanger is formed. The thickness of the corrugated plate is specified to 0.01-0.8 mm, preferably 0.05-0.5 mm. The pitch of the corrugation is preferably specified to 2-6 mm.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、熱交換器及びその
製造方法に関する。特に、内管に高速の高温ガス(気
体)を、外管に冷却水(液体)を通過させて熱交換を行
う熱交換器、例えば、内燃機関の排気ガスを冷却水によ
り冷却する排気冷却器(高度の熱交換能が要求される)
等に好適な発明である。
[0001] The present invention relates to a heat exchanger and a method for manufacturing the same. In particular, a heat exchanger that exchanges heat by passing high-speed high-temperature gas (gas) through the inner pipe and cooling water (liquid) through the outer pipe, for example, an exhaust cooler that cools exhaust gas of an internal combustion engine with cooling water (High heat exchange capacity is required)
This is a preferred invention.

【0002】ここでは、二重管式熱交換器を例に採り説
明するが、これに限られるものではない。
Here, a double-pipe heat exchanger will be described as an example, but the present invention is not limited to this.

【0003】[0003]

【背景技術】二重管式熱交換器としては、図1・2に示
す如く、内管12を外管14に挿通させ、外管14の両
端部を内管12の外壁に溶接したものがある。外管14
の両端部には、冷却水の入口ノズル16及び出口ノズル
18を向流/並流使用できるように形成されている(図
例では向流)。なお、20は管フランジである。
2. Description of the Related Art As shown in FIGS. 1 and 2, a double-pipe heat exchanger is one in which an inner pipe 12 is inserted into an outer pipe 14 and both ends of the outer pipe 14 are welded to the outer wall of the inner pipe 12. is there. Outer tube 14
The cooling water inlet nozzle 16 and outlet nozzle 18 are formed at both ends so that they can be used in countercurrent / cocurrent (countercurrent in the example in the figure). In addition, 20 is a pipe flange.

【0004】図1・2に示すような構成では、熱交換が
内管12の壁面だけであり、伝熱面積が小さく、かつ、
内管12の中心部側を流れる流体の熱交換が行い難く熱
交換効率が低い。即ち、全体として大きな熱交換能を得
難かった。
In the configuration shown in FIGS. 1 and 2, heat exchange is performed only on the wall surface of the inner tube 12, the heat transfer area is small, and
Heat exchange of the fluid flowing through the center of the inner tube 12 is difficult, and the heat exchange efficiency is low. That is, it was difficult to obtain a large heat exchange capacity as a whole.

【0005】このため、図3・4に示すような、複数本
(図例では4本)の細径の内管12Aを外管14の内側
に挿通させた多管式タイプが、通常、使用されている。
この構成では、伝熱面積が増大するとともに、中心部側
を流れる流体に対しても熱交換を行うことができ、大き
な熱交換能を得易い。
For this reason, as shown in FIGS. 3 and 4, a multi-tube type in which a plurality (four in the illustrated example) of small-diameter inner tubes 12A are inserted into the outer tube 14 is usually used. Have been.
With this configuration, the heat transfer area is increased, and heat exchange can be performed with respect to the fluid flowing on the central portion side, so that a large heat exchange capability is easily obtained.

【0006】しかし、図3・4に示す多管式タイプのも
のでは、製造工数がかさみ、かつ、重量も増大する傾向
にある。
However, the multi-tube type shown in FIGS. 3 and 4 tends to increase the number of manufacturing steps and increase the weight.

【0007】このため、本願発明者らは、先に、図1・
2に示す構成の二重管式熱交換器において、図5に示す
如く、内管12に、横断面放射状の波形チューブで形成
された伝熱フィン22を、内管12の管壁内側に接して
配した熱交換器を提案した(特願平9−182571号
(平成9年7月8日出願):特開平 −号公報参照、出
願時未公開)。伝熱面積の増大と内管12の中心部を流
れる流体の熱交換も可能として、熱交換能を増大させ
る。
[0007] For this reason, the inventors of the present invention have previously described FIG.
In the double-pipe heat exchanger having the configuration shown in FIG. 2, a heat transfer fin 22 formed of a corrugated tube having a radial cross section is brought into contact with the inner pipe 12 as shown in FIG. (Japanese Patent Application No. Hei 9-182571 (filed on Jul. 8, 1997): see Japanese Patent Application Laid-Open No. Hei 9 (1998), not disclosed at the time of filing). The heat transfer area can be increased and the fluid flowing through the center of the inner tube 12 can be exchanged with heat, thereby increasing the heat exchange capacity.

【0008】図5に示す構成の熱交換器において、伝熱
フィン22は、図6に示すような所定ピッチP及び所定
高さHで所定長さに裁断された波板24を巻いて管状に
したものを、内管(熱交換管体)12の管壁に波頂部2
5外側を接触させて配し、該波頂部外側をロウ付けして
固定していた。
In the heat exchanger having the structure shown in FIG. 5, the heat transfer fins 22 are formed by winding a corrugated sheet 24 cut into a predetermined length at a predetermined pitch P and a predetermined height H as shown in FIG. The crest 2 is placed on the wall of the inner tube (heat exchange tube) 12.
The outer side of the crest was fixed by brazing.

【0009】[0009]

【発明が解決しようとする課題】そして、上記ロウ付け
は、前記波頂部25の外側に、ロウ材(ペースト状)を
塗布して、前記伝熱フィン22を熱交換管体12に挿入
した熱交換器半製品を、ロウ付け加熱炉に投入し、所定
時間経過後、取り出して行っていた。
The brazing is performed by applying a brazing material (paste) to the outside of the crest 25 and inserting the heat transfer fins 22 into the heat exchange tube 12. The semi-finished exchanger was put into a brazing heating furnace, and was taken out after a lapse of a predetermined time.

【0010】しかし、このロウ付け方法の場合、伝熱フ
ィン22の波頂部25と熱交換管体12の管壁との間
に、安定したロウ付け性・ロウ付け強度が得られないこ
とが分かった。
However, in the case of this brazing method, it is found that stable brazing properties and brazing strength cannot be obtained between the crests 25 of the heat transfer fins 22 and the tube wall of the heat exchange tube 12. Was.

【0011】本発明は、上記にかんがみて、伝熱フィン
のロウ付け性・ロウ付け強度が安定して得られる熱交換
器及びその製造方法を提供することを目的とする。
SUMMARY OF THE INVENTION In view of the above, it is an object of the present invention to provide a heat exchanger in which the brazing property and brazing strength of a heat transfer fin can be stably obtained, and a method of manufacturing the same.

【0012】[0012]

【課題を解決するための手段】本発明者らは、上記課題
を解決するために、鋭意開発に努力をする過程で、上記
製造方法では、波頂部25の外側に塗布したロウ材が、
内管12へ挿入時に、内管12の内壁面と干渉して部分
的に移動又は寄せられたり脱落したりするとともに、伝
熱フィン22の波頂部25と熱交換管体12管壁との接
触隙間に流入せず、むしろ、他部に流下するためである
ことが分かり、下記構成の熱交換器及びその製造方法に
想到した。
Means for Solving the Problems In order to solve the above-mentioned problems, the present inventors have made intensive efforts for development, and in the above-mentioned manufacturing method, the brazing material applied to the outside of the crest 25 is
At the time of insertion into the inner tube 12, it partially interferes with the inner wall surface of the inner tube 12, or is moved or dropped, and at the same time, the crests 25 of the heat transfer fins 22 contact with the heat exchange tube 12 tube wall. It was found that the heat exchanger did not flow into the gap, but rather flowed down to the other part. Thus, a heat exchanger having the following structure and a method for manufacturing the same were conceived.

【0013】本発明の熱交換器は、所定高さ・所定ピッ
チで所定長さの波板を波方向に巻いて環状にした伝熱フ
ィンが、熱交換管体の管壁の内側若しくは外側又は二重
管で形成される環状空間の対向管壁に波頂部外側を接触
させて配され、該波頂部外側がロウ付けされてなる熱交
換器において、伝熱フィンの管壁と接触する波頂部外側
にロウ材保持溝が形成されていることを特徴とする。
In the heat exchanger according to the present invention, the heat transfer fins formed by winding a corrugated sheet of a predetermined length at a predetermined height and a predetermined pitch in a wave direction are formed inside or outside the tube wall of the heat exchange tube or In a heat exchanger in which the outer side of the crest is placed in contact with the opposite tube wall of the annular space formed by the double tube and the outer side of the crest is brazed, the crest that contacts the tube wall of the heat transfer fin A brazing material holding groove is formed on the outside.

【0014】上記熱交換器において、ロウ材保持溝が形
成されている波頂部が、接触する管壁の面接触可能な平
板状に形成されていることが望ましい。
In the above heat exchanger, it is desirable that the wave crest portion on which the brazing material holding groove is formed is formed in a flat plate shape capable of making surface contact with the tube wall to be contacted.

【0015】本発明の熱交換器の製造方法は、所定高さ
・所定ピッチで所定長さの波板を波方向に巻いて環状に
した伝熱フィンを、熱交換管体の管壁の内側若しくは外
側又は二重管で形成される環状空間の対向管壁に波頂部
外側を接触させて配し、該波頂部外側をロウ付けして製
造する工程を含む熱交換器の製造方法において、伝熱フ
ィンの管壁と接触する波頂部外側にロウ材保持溝を形成
するとともに、伝熱フィンを熱交換管体に接触させて配
する前工程で、ロウ材保持溝にロウ材を保持させること
を特徴とする。
According to the method of manufacturing a heat exchanger of the present invention, a heat transfer fin formed by winding a corrugated sheet of a predetermined length and a predetermined pitch in a wave direction at a predetermined height and a predetermined pitch is formed inside the pipe wall of the heat exchange pipe. Alternatively, in a method for manufacturing a heat exchanger, the method includes a step of arranging an outer side of a crest in contact with an outer tube wall of an annular space formed by an outer or double pipe and brazing the outer side of the crest. A brazing material holding groove is formed outside the wave crest in contact with the tube wall of the heat fin, and the brazing material is held in the brazing material holding groove in a process prior to disposing the heat transfer fin in contact with the heat exchange tube. It is characterized by.

【0016】上記熱交換器の製造方法において、ロウ材
保持溝を、波頂部を管壁の面接触可能に平板状にプレス
成形すると同時に形成することが望ましい。
In the method for manufacturing a heat exchanger, the brazing material holding groove is desirably formed at the same time that the crest is press-formed into a flat plate shape so that the crest can come into surface contact with the tube wall.

【0017】[0017]

【発明の作用・効果】本発明の熱交換器及びその製造方
法は、熱交換管体とロウ付けされる伝熱フィンの波頂部
外側にロウ材保持溝を形成することにより、該ロウ材保
持溝にロウ材を塗布若しくは棒状ロウ材をセットした状
態で伝熱フィンを熱交換管体にセットすることができ
る。
The heat exchanger and the method of manufacturing the same according to the present invention are characterized in that the brazing material holding groove is formed outside the wave crest of the heat transfer fin to be brazed to the heat exchange tube. The heat transfer fins can be set on the heat exchange tube in a state where the brazing material is applied to the grooves or the bar-shaped brazing material is set.

【0018】このため、ロウ付け加熱工程において、ロ
ウ材は、ロウ材保持溝の両側に形成される波頂部と管壁
との接触部隙間に流入する。このため、安定したロウ付
け性ロウ付け強度を確保できる。
For this reason, in the brazing and heating step, the brazing material flows into the contact gap between the crests formed on both sides of the brazing material holding groove and the tube wall. Therefore, stable brazing properties can be ensured.

【0019】特に、ロウ材保持溝が形成されている波頂
部を、接触する管壁の面接触可能に平板状に形成するこ
とにより、ロウ付け面積が確保し易く、より安定したロ
ウ付け性及びロウ付け強度を確保し易い。
In particular, by forming the crest where the brazing material holding groove is formed into a flat plate shape so that the surface of the contacting tube wall can be brought into contact, the brazing area can be easily secured, and more stable brazing property and Easy to secure brazing strength.

【0020】[0020]

【発明の実施の形態】以下、本発明の実施形態を図例に
基づいて説明をする。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.

【0021】(1) 図7に示すような波板26を、図8に
示すように熱交換管体(内管)28にロウ付け固定して
伝熱フィン30とする場合を例に採り説明する。図8の
断面図では、外管を省略してある。
(1) A case where a corrugated plate 26 as shown in FIG. 7 is brazed and fixed to a heat exchange tube (inner tube) 28 as shown in FIG. I do. In the sectional view of FIG. 8, the outer tube is omitted.

【0022】波板26は、ロウ付け面側(外周面となる
側)となる波頂部27の両側に曲げ部を備えたU字曲げ
部(第一曲げ形状)Uとされ、内周面側となる面側がV
字曲げ部(第二曲げ形状)Vとされている。
The corrugated plate 26 is formed as a U-shaped bent portion (first bent shape) U having bent portions on both sides of a crest portion 27 on the brazing surface side (the outer circumferential surface side), and the inner circumferential surface side. V side
A bent portion (second bent shape) V is formed.

【0023】当該波板26の調製方法は、特に限定され
ず、慣用の方法で調製できる。引き抜き等、波型のダイ
上を歯車状ポンチを転がして成形してもよいが、通常、
図9に示す如く、上型(押し型)32と下型(受け型)
34とを、プレス機にセットして、金属帯板(素材)3
6を順送り(シリンダ等で一段づつ持ち上げて定尺送り
する)して成形することが、所定ピッチの波板が正確に
成形できて望ましい。
The method of preparing the corrugated plate 26 is not particularly limited, and can be prepared by a conventional method. Rolling a gear-shaped punch on a corrugated die, such as drawing, may be performed, but usually,
As shown in FIG. 9, the upper die (push die) 32 and the lower die (receiving die)
34 is set on a press machine, and a metal strip (material) 3
It is desirable to form 6 by sequentially feeding (lifting up by one step by a cylinder or the like and feeding by a fixed length) so that a corrugated sheet of a predetermined pitch can be accurately formed.

【0024】このとき、本実施形態では、上型32と下
型34との間に、ロウ材保持溝形成用の凸条32aおよ
び凹条34aが形成されており、波頂部成形時に同時的
にロウ材保持溝29が形成可能とされている。
At this time, in the present embodiment, the convex ridge 32a and the concave ridge 34a for forming the brazing material holding groove are formed between the upper die 32 and the lower die 34. The brazing material holding groove 29 can be formed.

【0025】このときのロウ材保持溝29の断面形状
は、矩形、台形、三角形等、限定されないが、半円状の
ものを使用することが材料切れを発生させない見地から
望ましい。このときのRの大きさは、即ち、ロウ材保持
溝29のR(深さ)は、波形頂部27の大きさ等により
異なるが、0.2〜0.8mm、望ましくは、0.3〜
0.5mmとする。
The cross-sectional shape of the brazing material holding groove 29 at this time is not limited to a rectangle, a trapezoid, a triangle, or the like, but it is preferable to use a semi-circular shape from the viewpoint of preventing material cut. The magnitude of R at this time, that is, the R (depth) of the brazing material holding groove 29 varies depending on the size of the corrugated top 27 and the like, but is 0.2 to 0.8 mm, preferably 0.3 to 0.8 mm.
0.5 mm.

【0026】ここでは、ロウ付け面側がU字曲げ部とし
たが、通常の、図6に示すようなV字曲げ部のみの波板
またはU字曲げ部のみの波板でも同様である。
Here, the U-shaped bent portion is used on the brazing surface side. However, the same applies to a normal corrugated plate having only a V-shaped bent portion or a corrugated plate having only a U-shaped bent portion as shown in FIG.

【0027】上記のようにしてプレス成形した波板26
の巻き成形は、熱交換管体28例えば、ロウ付け側とは
反対側のV字形曲げ部を図10に示す如く、一段づつ、
突き曲げ成形により拡開して行うことが望ましい。
The corrugated sheet 26 press-formed as described above
As shown in FIG. 10, the winding forming of the heat exchange tube body 28, for example, a V-shaped bent portion on the side opposite to the brazing side is performed step by step.
It is desirable to perform the expansion by projecting and bending.

【0028】この突き曲げ成形は、例えば、図11に示
すような、上型(ポンチ)52と下型(ダイ)54とで
行う。即ち、上型52は、ポンチブロック52aとポン
チ部52bとからなり、下型54は、ダイブロック54
aと首部54cを介して二又ダイ部54bとからなる。
This bend forming is performed by, for example, an upper die (punch) 52 and a lower die (die) 54 as shown in FIG. That is, the upper mold 52 includes a punch block 52a and a punch portion 52b, and the lower mold 54 includes a die block 54.
a and a bifurcated die 54b via a neck 54c.

【0029】次に、上記巻き成形した伝熱フィン30の
波頂部(U字曲げ部Uの外側面)27にロウ材36、3
6Aを、塗布ないしセットする。即ち、ロウ材保持溝2
9に、ペースト状ロウ材36を図12に示す如く充填す
るか、又は、棒状ロウ材(例えば銅線)を図13に示す
如く嵌着する。棒状ロウ材36Aの場合は、ロウ材保持
溝29に締まり嵌め的に嵌着するよう保持溝のRより大
きめの直径(例えば2R+0.1mm)の棒材を使用する
ことが望ましい。棒状ロウ材36Aが脱落し難くなるた
めである。
Next, the brazing material 36, 3 is attached to the crest (outer side surface of the U-shaped bent portion U) 27 of the wound heat transfer fin 30.
6A is applied or set. That is, the brazing material holding groove 2
9 is filled with a paste brazing material 36 as shown in FIG. 12, or a bar brazing material (for example, copper wire) is fitted as shown in FIG. In the case of the bar-shaped brazing material 36A, it is desirable to use a bar material having a diameter (for example, 2R + 0.1 mm) larger than R of the holding groove so as to be fitted into the brazing material holding groove 29 in a tight fit. This is because the rod-shaped brazing material 36A becomes difficult to fall off.

【0030】こうしたロウ材36、36Aがセットされ
た伝熱フィン30を、熱交換管体28に従来と同様挿入
する。この際、ロウ材は保持溝に保持されているため、
熱交換管体28の管壁に接触しても、ロウ材が移動・脱
落するおそれがない。
The heat transfer fins 30 on which the brazing materials 36 and 36A are set are inserted into the heat exchange tube 28 as in the conventional case. At this time, since the brazing material is held in the holding groove,
Even if it comes into contact with the tube wall of the heat exchange tube 28, there is no possibility that the brazing material will move or fall off.

【0031】そして、伝熱フィン30はスプリングバッ
クにより、熱交換管体28の内側に密接状態となる。こ
の状態で、ロウ付け加熱炉を通過させることにより、熱
交換器のロウ付けが工程が完了する。
Then, the heat transfer fins 30 are brought into close contact with the inside of the heat exchange tube 28 by springback. In this state, the brazing of the heat exchanger is completed by passing through a brazing heating furnace.

【0032】このとき、ロウ付け加熱時においては、溶
融ロウ材は保持溝両側の管壁接触部との隙間に流入す
る。このため、安定したロウ付け強度を確保できる。
At this time, at the time of brazing and heating, the molten brazing material flows into the gap between the holding groove and the tube wall contact portions. Therefore, stable brazing strength can be secured.

【0033】なお、波板26の板厚は、材質により異な
るが、鋼製の場合、通常、0.01〜0.8mm、望まし
くは、0.05〜0.5mmとする。薄くしすぎると、形
態保持性とともに伝熱抵抗が大きくなり、また、厚いと
重量増大につながり望ましくない。
The thickness of the corrugated sheet 26 varies depending on the material, but when it is made of steel, it is usually 0.01 to 0.8 mm, preferably 0.05 to 0.5 mm. If the thickness is too small, the heat transfer resistance is increased together with the shape retention, and if the thickness is too large, the weight increases, which is not desirable.

【0034】また、内管12の内半径rと波板24の高
さHとの関係は、内管12の内径にもよるが、内管12
の内径10〜50mmの範囲で、通常H/r=0.1〜
0.8、望ましくは、H/r=0.2〜0.7とする。
そして内径の範囲に対応して、波の山の高さはH=4〜
20mmとする。
The relationship between the inner radius r of the inner tube 12 and the height H of the corrugated plate 24 depends on the inner diameter of the inner tube 12.
H / r = 0.1 to 0.1 to 50 mm
0.8, desirably, H / r = 0.2 to 0.7.
And according to the range of the inner diameter, the height of the wave peak is H = 4 ~
20 mm.

【0035】また、波板26の波ピッチは、要求伝熱面
積に対応して2〜6mmとする。
The wave pitch of the corrugated plate 26 is set to 2 to 6 mm corresponding to the required heat transfer area.

【0036】また、熱交換管体(内管)12、14、2
8の肉厚は、伝熱性の見地から可及的に薄い方が望まし
いが、伝熱フィン30に比して剛性が要求されるため、
伝熱フィンより厚肉とする。例えば、内管12の内径が
上記範囲の場合、通常0.1〜1.0mm、望ましくは
0.3〜0.8mmとする。
The heat exchange tubes (inner tubes) 12, 14, 2
8 is desirably as thin as possible from the viewpoint of heat transfer, but since rigidity is required as compared with the heat transfer fins 30,
Be thicker than the heat transfer fins. For example, when the inner diameter of the inner tube 12 is in the above range, it is usually 0.1 to 1.0 mm, preferably 0.3 to 0.8 mm.

【0037】なお、伝熱フィン30の配設部位は、熱交
換管体(内管)28の内側に限られず、図14に示す如
く、外周面でもよく、更には、図15に示すように二重
管12、14の環状部に設定してもよい。
The location of the heat transfer fins 30 is not limited to the inside of the heat exchange tube (inner tube) 28, but may be an outer peripheral surface as shown in FIG. 14, and further, as shown in FIG. It may be set in the annular portion of the double pipes 12, 14.

【図面の簡単な説明】[Brief description of the drawings]

【図1】従来の二重管式熱交換器を示す正面図FIG. 1 is a front view showing a conventional double tube heat exchanger.

【図2】図1の2−2線拡大断面図FIG. 2 is an enlarged sectional view taken along line 2-2 of FIG. 1;

【図3】従来の多管式熱交換器の一例を示す正面図FIG. 3 is a front view showing an example of a conventional multi-tube heat exchanger.

【図4】図3の4−4線断面図FIG. 4 is a sectional view taken along line 4-4 in FIG. 3;

【図5】図1において内管に波形チューブの伝熱フィン
を設けた図2に対応する拡大端面図
FIG. 5 is an enlarged end view corresponding to FIG. 2 in which a heat transfer fin of a corrugated tube is provided on the inner tube in FIG. 1;

【図6】波板の一例を示す斜視図FIG. 6 is a perspective view showing an example of a corrugated sheet.

【図7】本発明の適用すると好適な波板の一例を示す端
面図
FIG. 7 is an end view showing an example of a corrugated sheet suitable for applying the present invention.

【図8】図7の波板を熱交換管体に装着した状態を示す
端面図
FIG. 8 is an end view showing a state in which the corrugated sheet of FIG. 7 is mounted on a heat exchange tube.

【図9】図7の波板をプレス成形する場合の成形型を示
す断面図
9 is a cross-sectional view showing a forming die when the corrugated sheet of FIG. 7 is press-formed.

【図10】本発明の伝熱フィンを巻き成形する一態様を
示す説明図
FIG. 10 is an explanatory view showing one embodiment of winding and forming the heat transfer fin of the present invention.

【図11】波板を巻き成形する場合に使用する突き曲げ
型の断面斜視図
FIG. 11 is a cross-sectional perspective view of a punching die used for winding and forming a corrugated sheet.

【図12】本発明の伝熱フィンにおける波頂部へのロウ
材セットの一態様を示す斜視図
FIG. 12 is a perspective view showing one embodiment of a brazing material set on a crest in the heat transfer fin of the present invention.

【図13】同じく他のロウ材セット態様を示す斜視図FIG. 13 is a perspective view showing another brazing material setting mode.

【図14】伝熱フィンの他の組み付け態様を示す概略端
面図
FIG. 14 is a schematic end view showing another assembling mode of the heat transfer fin.

【図15】更に他の組み付け態様を示す概略端面図FIG. 15 is a schematic end view showing still another assembling mode.

【符号の説明】[Explanation of symbols]

12 内管 14 外管 22 伝熱フィン 24 波板 25 波頂部 26 波板 27 波頂部 28 熱交換管体 29 ロウ材保持溝 30 伝熱フィン 36、36A ロウ材 V V字形曲げ部 U U字形曲げ部 12 inner tube 14 outer tube 22 heat transfer fin 24 corrugated plate 25 crest 26 corrugated plate 27 crest 28 heat exchange tube 29 brazing material holding groove 30 heat transferring fin 36, 36A brazing material V V-shaped bending portion U U-shaped bending Department

フロントページの続き (72)発明者 北原 忠夫 愛知県名古屋市昭和区白金二丁目7番11号 マルヤス工業株式会社内 Fターム(参考) 3L103 AA01 AA11 BB17 CC02 CC27 DD08 DD34 DD38 Continuation of the front page (72) Inventor Tadao Kitahara 7-11 Shirokane, Showa-ku, Nagoya-shi, Aichi F-term in Maruyasu Kogyo Co., Ltd. 3L103 AA01 AA11 BB17 CC02 CC27 DD08 DD34 DD38

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 所定高さ・所定ピッチで所定長さの波板
を波方向に巻いて環状にした伝熱フィンが、熱交換管体
の管壁の内側若しくは外側又は二重管で形成される環状
空間の対向管壁に波頂部外側を接触させて配され、該波
頂部外側がロウ付けされてなる熱交換器において、 前記伝熱フィンの前記管壁と接触する波頂部外側にロウ
材保持溝が形成されていることを特徴とする熱交換器。
1. A heat transfer fin formed by winding a corrugated sheet of a predetermined length and a predetermined length in a wave direction at a predetermined height and a predetermined pitch into an annular shape inside or outside the heat exchange pipe wall or a double pipe. A heat exchanger in which the outer side of the crest is disposed in contact with the opposite tube wall of the annular space, and the outer side of the crest is brazed. A heat exchanger, wherein a holding groove is formed.
【請求項2】 前記ロウ材保持溝が形成されている波頂
部が、接触する管壁の面接触可能な平板状に形成されて
いることを特徴とする請求項1記載の熱交換器。
2. The heat exchanger according to claim 1, wherein the wave crest on which the brazing material holding groove is formed is formed in a flat plate shape capable of making surface contact with a tube wall to be contacted.
【請求項3】 所定高さ・所定ピッチで所定長さの波板
を波方向に巻いて環状にした伝熱フィンを、熱交換管体
の管壁の内側若しくは外側又は二重管で形成される環状
空間の対向管壁に波頂部外側を接触させて配し、該波頂
部外側をロウ付けして製造する工程を含む熱交換器の製
造方法において、 前記伝熱フィンの前記管壁と接触する波頂部外側にロウ
材保持溝を形成するとともに、前記伝熱フィンを前記熱
交換管体に接触させて配する前に、前記ロウ材保持溝に
ロウ材を保持させることを特徴とする熱交換器の製造方
法。
3. A heat transfer fin formed by winding a corrugated sheet of a predetermined length and a predetermined length in a wave direction at a predetermined height and a predetermined pitch into an annular shape inside or outside the heat exchange pipe wall or a double pipe. A method for manufacturing a heat exchanger, comprising the steps of: placing a crest outside on a facing tube wall of an annular space in contact with an annular space; and brazing the outside of the crest to manufacture the heat transfer fin. Forming a brazing material holding groove on the outer side of the wave crest, and holding the brazing material in the brazing material holding groove before disposing the heat transfer fins in contact with the heat exchange tube. Exchanger manufacturing method.
【請求項4】 前記ロウ材保持溝を、波頂部を管壁の面
接触可能に平板状にプレス成形すると同時に形成するこ
とを特徴とする請求項3記載の熱交換器。
4. The heat exchanger according to claim 3, wherein the brazing material holding groove is formed at the same time that the crest is press-formed into a flat plate shape so that the crest can come into surface contact with the tube wall.
JP10251686A 1998-09-07 1998-09-07 Heat exchanger Pending JP2000079462A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10251686A JP2000079462A (en) 1998-09-07 1998-09-07 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10251686A JP2000079462A (en) 1998-09-07 1998-09-07 Heat exchanger

Publications (1)

Publication Number Publication Date
JP2000079462A true JP2000079462A (en) 2000-03-21

Family

ID=17226510

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10251686A Pending JP2000079462A (en) 1998-09-07 1998-09-07 Heat exchanger

Country Status (1)

Country Link
JP (1) JP2000079462A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006035547A1 (en) * 2004-09-27 2006-04-06 Fujikin Incorporated Gas heating method and gas heating piping member
JP2008008549A (en) * 2006-06-29 2008-01-17 Kitayama Seisakusho:Kk Heat transfer tube and liquid heating device
WO2009063234A1 (en) * 2007-11-15 2009-05-22 Specialist Heat Exchangers Limited Thermal transfer apparatus, system and method
JP2010503817A (en) * 2006-09-19 2010-02-04 ベール ゲーエムベーハー ウント コー カーゲー Heat exchanger for internal combustion engines
KR101230499B1 (en) * 2012-08-28 2013-02-07 주식회사 성산 Heat transfer pipe having fin with closed cross section
JP2013143983A (en) * 2012-01-13 2013-07-25 Midori Anzen Co Ltd Heat pipe and liquid heater
WO2014054117A1 (en) * 2012-10-02 2014-04-10 三菱電機株式会社 Double-tube heat exchanger and refrigerating cycle device
KR101782824B1 (en) * 2013-06-20 2017-09-28 가부시키가이샤 무라타 세이사쿠쇼 Gas supply tube and heat processing device
KR101782825B1 (en) * 2013-06-20 2017-09-28 가부시키가이샤 무라타 세이사쿠쇼 Gas supply tube and heat processing device

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006035547A1 (en) * 2004-09-27 2006-04-06 Fujikin Incorporated Gas heating method and gas heating piping member
JP2008008549A (en) * 2006-06-29 2008-01-17 Kitayama Seisakusho:Kk Heat transfer tube and liquid heating device
JP2010503817A (en) * 2006-09-19 2010-02-04 ベール ゲーエムベーハー ウント コー カーゲー Heat exchanger for internal combustion engines
WO2009063234A1 (en) * 2007-11-15 2009-05-22 Specialist Heat Exchangers Limited Thermal transfer apparatus, system and method
JP2013143983A (en) * 2012-01-13 2013-07-25 Midori Anzen Co Ltd Heat pipe and liquid heater
KR101230499B1 (en) * 2012-08-28 2013-02-07 주식회사 성산 Heat transfer pipe having fin with closed cross section
WO2014054117A1 (en) * 2012-10-02 2014-04-10 三菱電機株式会社 Double-tube heat exchanger and refrigerating cycle device
WO2014054370A1 (en) * 2012-10-02 2014-04-10 三菱電機株式会社 Double-tube heat exchanger and refrigerating cycle device
CN104704311A (en) * 2012-10-02 2015-06-10 三菱电机株式会社 Double-tube heat exchanger and refrigerating cycle device
JP5944009B2 (en) * 2012-10-02 2016-07-05 三菱電機株式会社 Double tube heat exchanger and refrigeration cycle equipment
KR101782824B1 (en) * 2013-06-20 2017-09-28 가부시키가이샤 무라타 세이사쿠쇼 Gas supply tube and heat processing device
KR101782825B1 (en) * 2013-06-20 2017-09-28 가부시키가이샤 무라타 세이사쿠쇼 Gas supply tube and heat processing device

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